GLAND CONDENSER SKID SYSTEMS BY DIRECT CONTACT HEAT EXCHANGER TECHNOLOGY
20240084720 ยท 2024-03-14
Inventors
Cpc classification
F01K9/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01K9/003
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01D25/32
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F05D2220/31
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F05D2240/63
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01D25/183
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F05D2240/54
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01K11/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F01K11/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01K9/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
The disclosure concerns a gland condenser skid system comprising a direct contact heat exchanger as gland condenser, configured to collect and condensate steam coming from a steam turbine sealing system, wherein the steam turbine sealing system is provided with an air buffering seal device, separating steam turbine shaft lubricating oil system from the steam turbine sealing system.
Claims
1. A gland condenser system comprising a direct contact heat exchanger, configured to collect and condensate steam coming from a steam turbine sealing system, wherein the direct contact heat exchanger is a cylindrical column with a vertical axis, comprising an inlet for an air and steam mix flow from the steam turbine sealing system, in the lower part of the column and an inlet for cooling water at the top of the column, a condensate outlet at the bottom of the column and a residual steam and air outlet in the upper part of the column.
2. The gland condenser skid system according to claim 1, wherein the inlet for cooling water is provided with a spray nozzle.
3. The gland condenser skid system according to claim 1, wherein the residual steam and air outlet is connected to an evacuation device, configured as a vacuum generator.
4. The gland condenser skid system according to claim 3, wherein the evacuation device is a Venturi steam-operated pump fed by motive steam from a steam inlet.
5. The gland condenser skid system according to claim 3, wherein the evacuation device is connected downstream to a silencer.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0016] A more complete appreciation of the disclosed embodiments of the disclosure and many of the attended advantages thereof will be readily obtained as the same becomes better understood by reference to the following detailed description when considered in connection with the accompanying drawings, wherein:
[0017]
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[0022]
DETAILED DESCRIPTION OF EMBODIMENTS
[0023] According to one aspect, the present subject matter is directed to a gland condenser skid system comprising a direct contact heat exchanger as gland condenser.
[0024] According to another aspect, said gland condenser skid system being connected to a steam turbine provided with a seal buffering system to stop by air any possible contamination of the steam coming from the steam turbine sealing system and directed to the gland condenser.
[0025] Referring now to the drawings,
[0026]
[0027]
[0028]
[0029] Making reference to
[0030] Residual steam, together with air, is drawn through an outlet 24, in the higher zone of the direct contact gland condenser 20, and directed by an evacuation device 26 to a silencer 27 and thereafter to the atmosphere. Finally, the evacuation device is a vacuum generator and in particular a Venturi steam-operated pump fed by motive steam from a steam inlet 28.
[0031] The gland condenser skid system comprises pressure indicators 30 and a temperature indicator 31 and is supported by a structure 25 made of steel.
[0032] The gland condenser skid system including a gland condenser based on direct contact technology involves many advantages over a gland condenser based on shell and tubes technology, including: [0033] Simpler Geometry and Easier Fabrication, since direct contact heat exchanger solution is based on a simple vessel in which condensation occurs. No tube bundle presence is needed. [0034] More Compact and flexible lay-out, since direct contact heat exchanger type has a higher efficiency then traditional shell and tubes layout. Depending on specific needs, a proper design can be developed by optimization of easy to determine parameters, such as vessel diameter, length and flow direction. [0035] Lower installation because of reduced footprint due to vertical layout and lower maintenance costs, since the tube bundle absence strongly reduces any possible vessel damage during its life. [0036] Performance reliability, since a simpler system is able to guarantee heat efficiency. Upgrading of performance can be solved by sprayer substitution or easy cleaning. Moreover, any permanent performance reduction due to tubes fouling is removed. [0037] Reliable and cost-effective production in a variety of Petrochemical applications, with cost benefit compared to shell and tube solution in the range of 15-30% depending on materials and size classes. [0038] Full Materials applicability, ranging from carbon steel to stainless steel to Cu/Ni steel, depending on specific water typology. [0039] Compliance with major design and Fabrication codes, since pressure vessels codes can be applied without limitation. [0040] P&ID of gland system fully maintained vs Standard Approach, since no outlet cooling water line is necessary.
[0041] While aspects of the invention have been described in terms of various specific embodiments, it will be apparent to those of ordinary skill in the art that many modifications, changes, and omissions are possible without departing form the spirt and scope of the claims.